NUMERICAL-SIMULATION OF FLUID-FLOW AND HEAT-TRANSFER IN A SINGLE-SCREW EXTRUDER FOR NON-NEWTONIAN FLUIDS

被引:49
作者
KARWE, MV [1 ]
JALURIA, Y [1 ]
机构
[1] RUTGERS STATE UNIV,DEPT MECH & AEROSP ENGN,NEW BRUNSWICK,NJ 08903
关键词
D O I
10.1080/10407789008944738
中图分类号
O414.1 [热力学];
学科分类号
摘要
Thermal transport within the channel of a single-screw extruder has been studied numerically for non-Newtonian fluids, the computations art carried out for a given barrel temperature distribution and adiabatic screw. Numerical results are obtained using finite-difference techniques. The results indicate that the temperature variation in the downstream direction has a small effect on the corresponding velocity field, which is determined mainly by the total volume flow rate. It is also found that heat may be transferred from the flowing material to the barrel farther downstream under certain conditions. The residence time distribution is obtained numerically. Screw characteristics are presented in terms of bulk temperature rise versus screw speed.© 1990 by Hemisphere Publishing Corporation.
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页码:167 / 190
页数:24
相关论文
共 20 条
[1]  
AGUR EE, 1982, POLYM ENG SCI, V22, P1084, DOI 10.1002/pen.760221706
[2]   MIXING IN A SCREW EXTRUDER - MODEL FOR RESIDENCE TIME DISTRIBUTION AND STRAIN [J].
BIGG, D ;
MIDDLEMAN, S .
INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1974, 13 (01) :66-71
[3]  
Bruin S., 1978, Journal of Food Process Engineering, V2, P1, DOI 10.1111/j.1745-4530.1978.tb00193.x
[4]  
ELBIRLI B, 1984, POLYM ENG SCI, V24, P482, DOI 10.1002/pen.760240706
[5]   DEVELOPMENTS IN ANALYSIS OF STEADY SCREW EXTRUSION OF POLYMERS [J].
FENNER, RT .
POLYMER, 1977, 18 (06) :617-635
[6]  
FENNER RT, 1974, APR C ENG DES PLAST
[7]  
FENNER RT, 1980, PRINCIPLES POLYM PRO
[8]  
Griffith R.M, 1972, IND ENG CHEM FUND, V1, P181
[9]  
Harper J. M, 1980, FOOD EXTRUSION
[10]  
Jaluria Y., 1986, COMPUTATIONAL HEAT T